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JPH0578309B2 - - Google Patents
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JPH0578309B2 - - Google Patents

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Publication number
JPH0578309B2
JPH0578309B2 JP1035343A JP3534389A JPH0578309B2 JP H0578309 B2 JPH0578309 B2 JP H0578309B2 JP 1035343 A JP1035343 A JP 1035343A JP 3534389 A JP3534389 A JP 3534389A JP H0578309 B2 JPH0578309 B2 JP H0578309B2
Authority
JP
Japan
Prior art keywords
culture
fermentation
suspension
residue
acidic conditions
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP1035343A
Other languages
Japanese (ja)
Other versions
JPH02215387A (en
Inventor
Ryuichiro Kurane
Eiichi Mikami
Yasuhiro Nobata
Juko Yonemura
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hakuto Co Ltd
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
Hakuto Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Agency of Industrial Science and Technology, Hakuto Chemical Co Ltd filed Critical Agency of Industrial Science and Technology
Priority to JP1035343A priority Critical patent/JPH02215387A/en
Publication of JPH02215387A publication Critical patent/JPH02215387A/en
Publication of JPH0578309B2 publication Critical patent/JPH0578309B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/80Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
    • Y02P60/87Re-use of by-products of food processing for fodder production

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Fodder In General (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

1 技術/分野 本発明はロードコツカス・エリスロポレス(旧
名;ノカルデイア・エリスロポレス)KR−S−
1株(FERM P3530号)に代表されるように、
凝集剤生産能力を有するロードコツカス
(Rhodococcus)属細菌を培養して得られた培養
物又は培養処理物をカチオン系物質共存下又は酸
性条件下で発酵残基懸濁液と接触させて凝集さ
せ、有用物質を回収する方法に関するものであ
る。 2 従来技術 発酵残基懸濁液は、そのBOD(生物化学的酸素
要求量)の高さなどから、その後処理が困難な排
液の一つと言われている。しかしながら、その残
基懸濁液には非常に豊富な栄養源を含んでいるた
め、最近では例えばその飼料的価値が見直されて
きている。 古来、日本では酒造において酒発酵後に清澄の
ためのしぼり工程が取入れられ、その結果として
栄養価値の高い酒粕が副産物として形成され、そ
の一部は食用としてあるいはつけものなどに食生
活を豊かなものとしている。酒、ビールなどの発
酵液そのものをアルコールとして飲むものの他
に、ウイスキー、しようちゆうなどに代表される
蒸留酒もある。 これら蒸留酒発酵液においても蒸留液の残基懸
濁液には非常に豊富な栄養価値の高い資源が含ま
れている。これら蒸留後の残基懸濁液の一部は熱
濃縮などにより飼料として利用されているもの
の、ほとんどは従来の凝集剤による処理物の安全
性、処理時のPH調整の煩雑性やコスト面より手か
つけられておらず、活性汚泥処理によりあるいは
山林投棄、海洋投棄されてきている。 このような状況下、飼料輸入大国の我が国にお
いて、発酵残基懸濁液より飼料用などの価値の高
い有用成分を凝集回収し、飼料等として有効活用
できれば、高BOD排水のBOD除去処理と同時に
資源の再利用、リサイクル化が図られることにな
り、社会的に利するところは極めて大きいものが
あると考えられる。 3 発明が解決しようとする問題点 このような背景のもとに、飼料として安全に再
利用可能な有用物質を、発酵残基懸濁液等から簡
易で二次公害の恐れのない安全な処理方法を見出
すことにある。 4 問題点を解決するための手段 本発明者らが先に開発した微生物産生凝集剤
NOC−1(特許第1096062号)が、すぐれた効果
を有することを見出し、本発明を完成するに至つ
た。 即ち、本発明によれば、ロードコツカス属に属
し、凝集能力を有する微生物を培養して得られた
培養物及び/又は培養処理物をカチオン系物質共
存下あるいは酸性条件下で、発酵残基液等と接触
させることを特徴とする微生物産生凝集剤による
アルコール発酵残基懸濁液等の凝集回収方法が提
供される。 本発明に使用される菌株は、ロードコツカス属
に属し、凝集能を有する菌株であればよいが、そ
の代表例示菌株として、ロードコツカス・エリス
ロポレス(旧名;ノカルデイア・エリスロポレ
ス)KR−S−1株(FERM P3530号)が寄託さ
れている。なお、旧名;ノカルデイア・エリスロ
ポレスは1980年に国際微生物命名規約委員会によ
り、ロードコツカス・エリスロポレスに再整理・
再分類されている。 このような菌株の培地としては、グルコース、
フラクトース等の炭素源、尿素、硫安等の無機窒
素源、酵母エキス等の有機窒素源、その他、無機
塩類、ビタミン類等の栄養源が使用される。 培養は液体培養でも固体培養でもよい。通常は
通気攪拌液体培養で行う。培養は初発PHがPH4〜
11、温度20〜40℃の範囲で行われる。 約2日〜1週間で培養を終了し、凝集能を有す
る培養物を得ることができる。遠心分離等により
菌株を除去した上清液より、硫安沈殿等により凝
集物質を分離し、培養処理物を回収できる。本発
明では、このように精製した培養処理物を使用す
るまでもなく、培養物そのものを使用してもよ
く、また菌体自体も凝集能を有するため、そのま
ま使用することができる。 本発明で用いるコードコツカス属微生物が非病
原性であることは、バージー・マニユアル・シス
テマテツク・バクテリオロジー第2巻、
(Bergey's Manual of Systematic
Bacteriology Vol.2),1472〜1478頁、及びアグ
リカルチユラルバイオロジカル ケミストリー41
巻,(Agric.Biol.Chem.Vol.41),1031〜1038頁に
記載されている。従つて、本発明で凝集回収され
た有用物質は飼料安全法の規格を充分に満足する
ものである。 本発明においては、前記のようにして得られた
培養物及び/又は培養処理物と発酵残基懸濁液等
とを接触させて残基液中の有用資源物を凝集させ
るが、この場合カチオン系物質を添加することに
より、あるいは酸性下で接触させることにより、
より効果的な凝集回収を実施することができる。
なお、カチオン系物質としては、好ましくは2価
以上の多価カチオンを生成する化合物がよく、例
えば、塩化カルシウム、塩化アルミニウム、塩化
マグネシウム、塩化マンガン等が有利に用いられ
る。 本発明の方法は、一般的には発酵残基懸濁液に
本発明の方法に用いる培養物及び/又は培養処理
物を添加し、次いでカチオン系物質を添加する
が、あるいは酸性条件下、好ましくはPH5以下に
することにより実施されるがその実施方法は特に
制約されるものではない。このようにして得られ
た凝集回収物は栄養価の高い飼料等として使用で
きる。 本発明の対象とする発酵残基懸濁液が生ずる例
としは、アルコール発酵(工業用アルコール、ウ
イスキー、ビール、酒、しようちゆう等の製造)、
アミノ酸発酵(グルタミン酸、セリン、調味料、
メチオニン、イソロイシン等の製造)、抗生物質
発酵(ペニシリン、ストレプトマイシン、カナマ
イシン等の製造)、核酸発酵(イノシン酸等の製
造)、酵素発酵(アミラーゼ、プロテアーゼ、リ
パーゼ等の製造)、有機酸発酵(乳酸、クエン酸
等の製造)等がある。 5 実施例 次に本発明を実施例によりさらに詳細に説明す
る。 なお、SS(懸濁物質)、COD(化学的酸素要求
量)、SV30(30分静置後の汚泥容積指標)はいず
れもJIS規格に従つて測定した。 また、以下の実施例において用いた微生物産生
凝集剤NOC−1は次のようにして得られたもの
である。 グルコース5g、フラクトース5g、KH2PO4
2g、K2HPO45g、MgSO40.2g、尿素0.5g、
酵母エキス0.5gを蒸留水1に溶かし、培地の
PHを8.0に調整した培地100mlを300mlの三角フラ
スコにとり、オートクレープにより120℃、15分
間無菌殺菌した後、ロードコツカス・エリスロポ
レス(旧名;ノカルデイア・エリスロポレス)
KR−S−1株(FERM P3530号)を1白金耳の
量でフラスコに移植する。30℃にてロータリー
(回転)培養を行い、4〜5日間培養して培養物
を得た。この培養物より冷却遠心により菌体を除
去した遠心上清液に、0.8飽和になるように硫安
を添加する。硫安沈澱物を集め透析膜(Visking
チユーブ)にて透析を行い、その後透析内液を凍
結乾燥等により粘着性のある生成物である培養処
理物を得ることができる。この培養処理物は使用
前に再び蒸留水等に溶かして使用する。 [実施例 1] ウイスキー発酵蒸留残基液400mlを500mlビーカ
ーに入れ、20mm×40mmの羽根板を備えた攪拌機に
て毎分150回転にて、前記の培養物を最終濃度
5000ppmあるいは培養処理物を最終濃度500ppm
になるように添加した後、PH調整を酢酸(又は塩
酸)にて3.9に調整し、さらに5分間攪拌を続け
た。反応液を30分静置させた後、反応液のSV30
及び上澄液のCOD及びSSを測定した。 なお、比較のため、培養物(又は培養処理物)
を添加してないコントロール区を上述の方法に従
つて測定した。 結果を表1に示す。
1 Technology/Field The present invention relates to Rhodococcus erythropores (former name: Nocardia erythropores) KR-S-
As represented by 1 share (FERM P3530),
A culture obtained by culturing Rhodococcus bacteria capable of producing a flocculant or a culture-treated product is brought into contact with a fermentation residue suspension in the coexistence of a cationic substance or under acidic conditions to flocculate it, and the resulting product is useful. It concerns a method for recovering materials. 2. Prior Art Fermentation residue suspension is said to be one of the waste fluids that is difficult to process afterwards due to its high BOD (biochemical oxygen demand). However, since the residue suspension contains an extremely rich nutrient source, its value as feed, for example, has recently been reconsidered. Since ancient times in Japan, sake brewers have adopted a squeezing process for clarification after fermentation, resulting in the formation of highly nutritious sake lees as a by-product, some of which is eaten as food or as a pickle to enrich the diet. There is. In addition to alcoholic beverages such as sake and beer, which are made from the fermented liquid itself, there are also distilled spirits such as whiskey and shochiyu. Even in these fermented spirits, the residue suspension of the distillate contains extremely rich resources with high nutritional value. Although some of the residue suspension after distillation is used as feed by thermal concentration, most of it is used due to the safety of the processed material using conventional flocculants, the complexity of PH adjustment during processing, and the cost. It is left untouched and has been treated with activated sludge, dumped in forests, or dumped into the ocean. Under these circumstances, in Japan, which is a major feed importer, if we can aggregate and collect valuable useful ingredients for feed, etc. from the fermented residue suspension and effectively use them as feed, we can simultaneously treat BOD removal from high BOD wastewater. Resources will be reused and recycled, and the social benefits are thought to be extremely large. 3. Problems to be solved by the invention Based on this background, useful substances that can be safely reused as feed can be processed from fermentation residue suspensions, etc. in a simple and safe manner without the risk of secondary pollution. It's about finding a way. 4 Means for solving the problem Microorganism-produced flocculant developed by the present inventors
It was discovered that NOC-1 (Patent No. 1096062) has excellent effects, and the present invention was completed. That is, according to the present invention, a culture and/or a culture-treated product obtained by culturing a microorganism belonging to the genus Rhodococchus and having a flocculating ability is treated with a fermentation residue liquid, etc. in the presence of a cationic substance or under acidic conditions. Provided is a method for flocculating and recovering a suspension of alcoholic fermentation residues using a microorganism-produced flocculant, which comprises bringing the suspension into contact with a microorganism-produced flocculant. The strain used in the present invention may be any strain that belongs to the genus Rhodococcus and has agglutinating ability, but a representative example of the strain is Rhodococcus erythropores (formerly known as Nocardia erythropores) KR-S-1 (FERM P3530). No.) has been deposited. The former name Nocardia erythropores was reorganized and reorganized into Rhodococcus erythropores by the International Committee on Nomenclature of Microorganisms in 1980.
It has been reclassified. Culture media for such strains include glucose,
Carbon sources such as fructose, inorganic nitrogen sources such as urea and ammonium sulfate, organic nitrogen sources such as yeast extract, and other nutritional sources such as inorganic salts and vitamins are used. Culture may be liquid culture or solid culture. It is usually carried out using aerated agitation liquid culture. Initial pH of culture is PH4 ~
11, carried out at a temperature range of 20-40℃. The culture can be completed in about 2 days to 1 week, and a culture having flocculation ability can be obtained. From the supernatant liquid from which bacterial strains have been removed by centrifugation or the like, aggregated substances can be separated by ammonium sulfate precipitation or the like, and the cultured product can be recovered. In the present invention, there is no need to use the culture product purified in this way, and the culture itself may be used, and since the bacterial cells themselves have aggregation ability, they can be used as they are. The fact that the microorganisms of the genus Cordococcus used in the present invention is non-pathogenic is described in Virgie Manual Systematic Bacteriology Vol. 2,
(Bergey's Manual of Systematic
Bacteriology Vol. 2), pp. 1472-1478, and Agricultural Biological Chemistry 41
Vol., (Agric.Biol.Chem.Vol.41), pages 1031-1038. Therefore, the useful substances coagulated and recovered in the present invention fully satisfy the specifications of the Feed Safety Act. In the present invention, the culture and/or culture-treated product obtained as described above is brought into contact with a fermentation residue suspension or the like to aggregate useful resources in the residue, but in this case, cations By adding a system substance or by contacting under acidic conditions,
More effective coagulation recovery can be performed.
The cationic substance is preferably a compound that generates a polyvalent cation of divalent or higher valence, and for example, calcium chloride, aluminum chloride, magnesium chloride, manganese chloride, etc. are advantageously used. In the method of the present invention, generally, the culture and/or culture treatment product used in the method of the present invention is added to the fermentation residue suspension, and then a cationic substance is added, or preferably under acidic conditions. This is carried out by reducing the pH to 5 or lower, but the method of carrying out is not particularly limited. The aggregates thus obtained can be used as highly nutritious feed, etc. Examples where the fermentation residue suspension that is the object of the present invention is produced include alcohol fermentation (manufacturing of industrial alcohol, whisky, beer, sake, sake, etc.);
Amino acid fermentation (glutamic acid, serine, seasoning,
(Production of methionine, isoleucine, etc.), antibiotic fermentation (Production of penicillin, streptomycin, kanamycin, etc.), Nucleic acid fermentation (Production of inosinic acid, etc.), Enzyme fermentation (Production of amylase, protease, lipase, etc.), Organic acid fermentation (Production of lactic acid, etc.) , production of citric acid, etc.). 5 Examples Next, the present invention will be explained in more detail using examples. Note that SS (suspended solids), COD (chemical oxygen demand), and SV 30 (sludge volume index after standing still for 30 minutes) were all measured according to JIS standards. Further, the microorganism-produced flocculant NOC-1 used in the following examples was obtained as follows. Glucose 5g, Fructose 5g, KH 2 PO 4
2g, K 2 HPO 4 5g, MgSO 4 0.2g, urea 0.5g,
Dissolve 0.5g of yeast extract in 1 part of distilled water and add to the culture medium.
Transfer 100 ml of the medium adjusted to pH 8.0 into a 300 ml Erlenmeyer flask, sterilize it by autoclaving at 120℃ for 15 minutes, and then transform it into Rhodococcus erythropores (former name: Nocardia erythropores).
One loopful of KR-S-1 strain (FERM P3530) is transplanted into a flask. Rotary culture was performed at 30°C for 4 to 5 days to obtain a culture. Cells were removed from this culture by cooling centrifugation, and ammonium sulfate was added to the centrifuged supernatant to give a saturation of 0.8. The ammonium sulfate precipitate is collected using a dialysis membrane (Visking).
Dialysis is performed in a tube), and then the cultured product, which is a sticky product, can be obtained by freeze-drying the dialyzed fluid. This cultured product is redissolved in distilled water or the like before use. [Example 1] 400 ml of whiskey fermentation distillation residue liquid was placed in a 500 ml beaker, and the above culture was brought to the final concentration using a stirrer equipped with a blade plate of 20 mm x 40 mm at 150 revolutions per minute.
5000ppm or culture treated product at final concentration 500ppm
After addition, the pH was adjusted to 3.9 with acetic acid (or hydrochloric acid), and stirring was continued for an additional 5 minutes. After allowing the reaction solution to stand still for 30 minutes, the SV 30 of the reaction solution
And the COD and SS of the supernatant were measured. For comparison, cultured products (or cultured products)
A control group to which no chloride was added was measured according to the method described above. The results are shown in Table 1.

【表】 ウイスキー発酵蒸留残基液にNOC−1(培養物
又は培養処理物)を酸性条件下にて接触させるこ
とにより、ウイスキー発酵蒸留残基液中にある有
用物を効果的に回収できることが判明した。 このようなウイスキー発酵残基懸濁液の一部
は、現在は熱濃縮により濃縮され、飼料化されて
いる。この濃縮工程に本凝集剤を使用することに
より、大幅なエネルギー消費の減少が図られるも
のと期待されることによりコスト面での寄与も期
待できる。 [実施例 2] 酒のしぼり工程後の粕を乳鉢にて良くすりつぶ
し、蒸留水に懸濁させ1w/v%液とした後、さ
らにホモゲナイザーにて均一に懸濁させることに
より、酒のしぼり工程前に近似した液を調整し
た。 100mlメスシリンダーにNOC−1(培養液)2
mlをとり蒸留水にて10mlにした後、このしぼり
粕調整懸濁液80mlを添加し、さらに蒸留水10mlを
加え、酢酸にてPHを3.9〜4.0に調整し、30分静置
させた後の上澄液のSSを測定した。 なお、対照区は培養液2mlの代りに蒸留水を用
いた。 結果を表2に示す。
[Table] By bringing NOC-1 (culture or culture-treated product) into contact with the whiskey fermentation and distillation residue under acidic conditions, useful substances in the whiskey fermentation and distillation residue can be effectively recovered. found. A portion of such a whiskey fermentation residue suspension is currently concentrated by thermal concentration and turned into feed. By using the present flocculant in this concentration step, it is expected that energy consumption will be significantly reduced, which can also be expected to contribute to cost reduction. [Example 2] The lees after the sake squeezing process were thoroughly ground in a mortar, suspended in distilled water to make a 1w/v% liquid, and then further suspended uniformly in a homogenizer to complete the sake squeezing process. A similar solution was prepared before. NOC-1 (culture solution) 2 in a 100ml graduated cylinder
After taking 1 ml and making it to 10 ml with distilled water, add 80 ml of this squeezed lees adjustment suspension, further add 10 ml of distilled water, adjust the pH to 3.9 to 4.0 with acetic acid, and let it stand for 30 minutes. The SS of the supernatant liquid was measured. Note that in the control group, distilled water was used instead of 2 ml of the culture solution. The results are shown in Table 2.

【表】 米を発酵させたしぼり粕の調整懸濁液にNOC
−1(培養物)を加え、凝集時のPHを酸性条件下
にすることにより、しぼり粕の微細懸濁物を凝集
沈澱させ、回収できることがわかつた。 [実施例 3] 実施例2において得られたしぼり粕調整懸濁液
の凝集反応時における条件を酸性下ではなく、カ
チオン系物質共存下で反応させることにより懸濁
液の凝集沈殿回収が可能かどうか検討した。 100mlメスシリンダーに、NOC−1(培養液)
2mlを入れ、蒸留水にて10mlにフイールアツプ
し、次いでしぼり粕調整懸濁液80mlを入れた後、
塩化カルシウム液(10%CaCl2液)10mlを加えよ
く混合させ混合液のPHを6.9〜7.0に調整する。30
分静置後の上澄液のCOD及びSSを測定し、調整
懸濁液の回収をみた。 結果を表3に示す。 表3に示す如く、カチオン系物質の共存下にて
接触させることにより、調整懸濁液のNOC−1
による凝集回収が可能であることがわかつた。
[Table] NOC in the adjusted suspension of fermented rice lees
It was found that by adding -1 (culture) and setting the pH at the time of aggregation to acidic conditions, a fine suspension of squeezed lees could be coagulated and precipitated and recovered. [Example 3] Is it possible to collect the flocculation and sedimentation of the suspension by changing the conditions during the flocculation reaction of the squeezed lees-adjusted suspension obtained in Example 2 to the coexistence of a cationic substance instead of under acidic conditions? Please consider it. NOC-1 (culture solution) in a 100ml graduated cylinder
After adding 2 ml and increasing the volume to 10 ml with distilled water, then adding 80 ml of the squeezed lees adjustment suspension,
Add 10 ml of calcium chloride solution ( 2 solutions of 10% CaCl), mix well, and adjust the pH of the mixture to 6.9 to 7.0. 30
The COD and SS of the supernatant liquid after standing for minutes were measured, and the recovery of the adjusted suspension was observed. The results are shown in Table 3. As shown in Table 3, by contacting in the presence of a cationic substance, the NOC-1 of the prepared suspension was
It was found that coagulation recovery is possible by

【表】 [実施例 4] しようちゆう製造粕である発酵バルクを10v/
v%になるように調整した。 培養処理物0.2mgを10mlの蒸留水に良く溶解さ
せた後、しようちゆう発酵バルク液80mlを加え、
さらに塩化カルシウム液(10%CaCl2液)10mlを
加え、凝集時のPHを6.9〜7.0に調整した。 対照区としては、培養処理物を含まない蒸留水
10mlを用いて同様な操作を行いコントロールとし
た。 凝集開始後30分静置後の上澄液のSSおよび
CODを測定した。 結果を表4に示す。
[Table] [Example 4] Fermented bulk, which is Shochiyu production lees, at 10v/
It was adjusted to be v%. After thoroughly dissolving 0.2 mg of the cultured product in 10 ml of distilled water, add 80 ml of Shochiyu fermentation bulk liquid.
Furthermore, 10 ml of calcium chloride solution ( 2 solutions of 10% CaCl) was added to adjust the pH at the time of aggregation to 6.9 to 7.0. As a control, distilled water without culture treatment was used.
A similar operation was performed using 10 ml to serve as a control. Supernatant liquid SS and
COD was measured. The results are shown in Table 4.

【表】 しようちゆう発酵蒸留粕(発酵バルク)にカチ
オン系物質共存下にて本凝集剤を作用させること
により、発酵蒸留粕水を凝集回収できることが示
された。 6 効果 以上に示した結果から示されるように、本凝集
剤を酸性条件下、好ましくはPH5以下、あるいは
カチオン系物質共存下にて発酵残基懸濁液と接触
させることにより、発酵残基懸濁液の簡易な処理
と同時に凝集沈澱回収による有用物質(飼料等)
の安全な再利用化が期待できることが明らかにな
つた。
[Table] It has been shown that fermentation distillation lees water can be coagulated and recovered by allowing this flocculant to act on fermented distillation lees (fermented bulk) in the presence of cationic substances. 6 Effects As shown by the results shown above, fermentation residue suspension can be improved by bringing this flocculant into contact with the fermentation residue suspension under acidic conditions, preferably at a pH of 5 or below, or in the presence of cationic substances. Useful substances (feed, etc.) by simple treatment of turbid liquid and collection of flocculation and sedimentation at the same time.
It has become clear that safe reuse of the materials can be expected.

Claims (1)

【特許請求の範囲】 1 ロードコツカス属(Rhodococcus)細菌培
養物及び/又はその処理物を主成分とする凝集剤
をカチオン系物質の共存下で発酵残査懸濁液と接
触させて有用物質を凝集回収する方法。 2 請求項1の培養物及び/又は培養処理物を酸
性条件下で発酵残基懸濁液と接触させて有用物質
を凝集回収する方法。
[Claims] 1. A flocculant containing a Rhodococcus bacterial culture and/or a processed product thereof as a main component is brought into contact with a fermentation residue suspension in the presence of a cationic substance to flocculate useful substances. How to collect. 2. A method for aggregating and recovering useful substances by bringing the culture and/or culture-treated product according to claim 1 into contact with a fermentation residue suspension under acidic conditions.
JP1035343A 1989-02-15 1989-02-15 Method for flocculating and recovering useful substance from fermentation residual suspension with flocculant produced by microorganism Granted JPH02215387A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1035343A JPH02215387A (en) 1989-02-15 1989-02-15 Method for flocculating and recovering useful substance from fermentation residual suspension with flocculant produced by microorganism

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1035343A JPH02215387A (en) 1989-02-15 1989-02-15 Method for flocculating and recovering useful substance from fermentation residual suspension with flocculant produced by microorganism

Publications (2)

Publication Number Publication Date
JPH02215387A JPH02215387A (en) 1990-08-28
JPH0578309B2 true JPH0578309B2 (en) 1993-10-28

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Country Status (1)

Country Link
JP (1) JPH02215387A (en)

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* Cited by examiner, † Cited by third party
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JP4780414B2 (en) * 2007-02-16 2011-09-28 サンコーテック株式会社 Liquid medium and method for growing and cultivating photosynthetic bacteria
JP5263768B2 (en) * 2008-10-15 2013-08-14 日鉄住金環境株式会社 Organic waste liquid treatment method

Also Published As

Publication number Publication date
JPH02215387A (en) 1990-08-28

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